Stability studies were undertaken at ambient (25ºC/60%RH) and accelerated conditions (40ºC/75%RH) to determine the effect of changing of hard gelatin capsule supplier on a phenytoin sodium (100 mg) capsule formulation. Three hard gelatin capsule suppliers: RP Scherer (Supplier A), Capsugel (supplier B) and Associated Caps (Supplier C) were used in the study. Capsules were analyzed just after filling of the capsules (T0), after 1 month (T1), after 2 months (T2) and after 3 months (T3) after being stored in securitainers under the above-mentioned conditions. The moisture content of the empty shells as well as the capsule contents were analysed at each time-point. The capsule disintegration time was recorded at each time point. Multi-point dissolution testing was performed at each time point to determine the release of the active substance in each case. Based on the achieved results, the best capsule shell supplier was recommended, and other suggestions were made to improve the capsule formulation.

Many Active Pharmaceutical Ingredients (API) such as the antiviral agent famciclovir (FCV) are required for paediatric treatment but are not commercially available in age-appropriate dosage forms. It is common practice to prepare oral liquid dosage forms using commercially available tablets, capsules or powdered API and then dispersing or dissolving the crushed and/or powdered materials in a vehicle that the patient can swallow. Vehicles that are commonly used for this purpose include methylcellulose, syrup or combinations of these carriers where possible or commercially available suspending agents such as Ora-Sweet®, if available, can be used. However, several critical factors are overlooked when manufacturing extemporaneous formulations including, but not limited to, physical and chemical properties of the API, excipients, compatibility, stability and bioavailability issues. A stability-indicating High Performance Liquid Chromatography (HPLC) method for the analysis of FCV was developed and validated according to the International Conference on Harmonization (ICH) guidelines. The method is sensitive, selective, precise, accurate and linear over the concentration range 2-120 μg/ml. The stability of 25 mg/ml FCV formulations was assessed in vehicles manufactured from syrup simplex, hydroxypropyl methylcellulose (HPMC), Ora-Sweet® and an aqueous buffer (pH 6) following storage at 25 °C/60% RH and 40 °C/75% RH over six (6) to eight (8) weeks. The shelf life of the products was calculated as the longest period of storage for approximately 90% of the added FCV to be recovered. Formulations were manufactured using syrup simplex or HPMC with methylparaben and propylparaben individually or in combination and with sodium metabisulphite, ascorbic acid or citric acid as antioxidants. The resultant products were subject to quality control analysis for API content, viscosity, pH and appearance and the resultant data were subject to statistical analysis. The degradation rates were calculated for each product and a degradation profile plotted. The degradation rates of FCV in extemporaneous formulations were compared to those of FCV manufactured using a commercially available suspending agent and a buffered vehicle. FCV undergoes major degradation in the presence of sucrose, as observed for formulations in which the vehicle was syrup and Ora-Sweet®. FCV was found to be most stable when dissolved/dispersed in an HPMC vehicle incorporating sodium metabisulphite and a combination of parabens. The formulation that exhibited the maximum stability was manufactured using an aqueous solution buffered to pH 6. Due to the enhanced stability of FCV when added to a buffered vehicle a formulation in which an HPMC vehicle buffered to pH 6 with sodium metabisulphite, methylparaben and propylparaben was selected for optimisation using a Central Composite Design approach (CCD). In this way it was possible to establish a relationship between input variables such as pH, % w/v HPMC, % w/v antioxidant and % w/v preservative and the responses selected for monitoring by means of response surface modelling. A quadratic model was found to be the most appropriate to describe the relationship between input and output variables. Thirty batches of product were randomly manufactured according to the CCD and analysed to establish the stability in respect of viscosity, pH and the amount of FCV remaining following storage and the data were fitted to models using Design-Expert® software. A correlation between input variables and the responses was best described by a quadratic polynomial model. Analysis of Variance indicated that the response surface models were significant (P-value < 0.0001). The pH to which a FCV formulation was buffered was the most significant factor to effect the % drug content and the ultimate pH of the formulation, while the % w/v HPMC had the most significant effect on the viscosity of the product. The optimum composition for the manufacture of an oral liquid FCV formulation was predicted using the optimisation function of the Design-Expert® software. A low % error of prediction was established, indicating that the model is robust and that RSM is an appropriate formulation optimisation tool as it has a high prognostic ability. A liquid FCV formulation was developed, optimised and found to be suitable for its intended purpose. However further optimisation is required in respect of colourants, sweeteners and/or flavourants. The approach followed is useful in ensuring the development of quality products and can be applied in future.

The use of minocycline for the treatment of a broad range of systemic infections and for severe acne has been associated with vestibular side effects. The severity of side effects may lead to poor adherence to therapy by patients. The use of sustained release formulations of minocycline that display slow dissolution of minocycline following administration may be beneficial in reducing the incidence and severity of side effects. Therefore, sustained release capsule dosage forms containing 100 mg minocycline (base) were manufactured and assessed for use as sustained release oral dosage forms of minocycline. Minocycline sustained release capsules were manufactured based on matrix technologies using hydroxypropylmethyl cellulose (HPMC) and Compritol® as release retarding polymers. The rate and extent of minocycline release from the capsules was evaluated using USP Apparatus 1 and samples were analysed using a validated High Performance Liquid Chromatographic (HPLC) method with ultraviolet (UV) detection. Differences in the rate and extent of minocycline release from formulations manufactured using HPMC or Compritol® were influenced by the concentration of polymer used in the formulations. The rate and extent of minocycline release was faster and greater when low concentrations of polymer were used in formulations. The effect of different excipients on the release pattern(s) of minocycline and particularly their potential to optimise minocycline release from experimental formulations was investigated. The use of diluents such as lactose and microcrystalline cellulose (MCC) revealed that lactose facilitated minocycline release when HPMC was used as the polymer matrix. In contrast, the use of lactose as diluent resulted in slower release of minocycline from Compritol® based formulations. The addition of sodium starch glycolate to HPMC based formulations resulted in slower release of minocycline than when no sodium starch glycolate was used. Compritol® based formulations were observed to release minocycline faster following addition of sodium starch glycolate and Poloxamer 188 to experimental formulations. In vitro dissolution profiles were compared to a target or reference profile using the difference and similarity factors, ƒ1 and ƒ2 , and a one way analysis of variance (ANOVA). In addition, the mechanism of minocycline release was elucidated following fitting of dissolution data to the Korsmeyer-Peppas, Higuchi and Zero order models. Minocycline release kinetics were best described by the Korsmeyer-Peppas model and the values of the release exponent, n (italics), revealed that drug release was a result of the combined effects of minocycline diffusion through matrices and erosion of the matrices. These in vitro dissolution profiles were better fit to the Higuchi model than to the Zero order model. Two formulations that displayed a fit to the Zero order model were identified for further studies as potential dosage forms for sustained release minocycline.

ABSTRACT<p><p>This project aimed at developing a drug delivery system (DDS) able to enhance the stability and<p>residence time in vivo of antibodies (Abs). The system will deliver drug by the subcutaneous<p>route (SC), while ensuring accurate control of the drug release and the resulting plasmatic level. This technology platform will allow to reduce frequency of injection, potentially decrease side effects and maintain high concentration of Abs which will improve life of patient having chronic disease such as autoimmune and inflammatory disease. Biodegradable synthetic polymer-based formulations (polylactide-co-glycolide (PLGA)) were selected as carriers for encapsulated Abs. This was because they offer good protection for the Abs and allow sustained release of the Abs for a controlled period of time. After the evaluation of different encapsulation methods such as the water-oil-in-water (w/o/w) and the solid-in-oil-inwater<p>(s/o/w) processes, the encapsulation of the Ab in solid state (s/o/w) appeared to be more appropriate for producing Ab-loaded PLGA microspheres (MS). It allowed us to maintain the<p>Ab in a monomeric conformation and to avoid the formation of unsoluble aggregates mainly present at the water/oil interface. The first part of the project was the optimization of both the method for producing the Ab solid particles (spray-drying process) and the encapsulation of these Ab solid particles into the polymeric MS (s/o/w process) by design of experiment (DoE). These optimizations were carried out using a bovine polyclonal immunoglobulin G (IgG) as model molecule. In further optimization of the spray-drying process by (DoE), aqueous Ab solutions were spray-dried using a mini Spray-Dryer assembly with a 0.7 mm spray nozzle. In accordance with the particle size (d(0.5) ~5 μm), the stability (no loss of monomer measured by<p>size exclusion chromatography (SEC) and the yield of the spray-drying process (> 60 % w/w), the process parameters were set of follow: 3 mL/min as liquid feed flow rate, 130°C /75°C as inlet temperature (inlet T°) / outlet temperature (outlet T°), 800 L/h as atomization flow rate and<p>30 m3/h as drying air flow rate. For the s/o/w, the methylene chloride (MC) commonly used for<p>an encapsulation process was replaced by ethyl acetate (EtAc), which was considered as a more<p>suitable organic solvent in terms of both environmental and human safety. The effects of several processes and formulation factors were evaluated on IgG:PLGA MS properties such as: particle size distribution, drug loading, IgG stability, and encapsulation efficiency (EE%). Several formulations and processing parameters were also statistically identified as critical to get reproducible process (e.g. the PLGA concentration, the volume of the external phase, the emulsification rate, and the quantity of IgG microparticles). The optimized encapsulation<p>method of the IgG has shown a drug loading of up to 6 % (w/w) and an encapsulation efficiency<p>of up to 60 % (w/w) while preserving the integrity of the encapsulated antibody. The produced MS were characterized by a d(0.9) lower than 110 μm and showed burst effect lower than 50 %(w/w). In the second part of the project, the optimized spray-drying and s/o/w processes<p>developed with the IgG were applied to a humanized anti-tumor necrosis factor (TNF) alpha<p>MAb to confirm the preservation of the MAb activity during these processes. The selected s/o/w method allowed us to produce MAb-loaded PLGA MS with an appropriate release profile up to 6 weeks and MAb stability. In order to maintain the Abs’ activity, both during encapsulation and<p>dissolution, the addition of a stabilizer such as trehalose appeared to be crucial, as did the<p>selection of the PLGA. It was demonstrated that the use of a PLGA characterized by a 75:25<p>lactide:glycolide (e.g. Resomer ® RG755S) ratio decreased the formation of low molecular weight species during dissolution, which led to preserve Abs activity through its release from the<p>delivery system. Furthermore, the release profile was adjusted according to the type of polymer<p>and its concentration. E.g. 10 % w/v RG755S allowed Ab MS with a release time of 6 weeks to<p>be obtained. The optimization of both the formulation and the encapsulation process allowed<p>maximum 13 % w/w Ab-loaded MS to be produced. It was demonstrated that the Ab-loaded PLGA MS were stable when stored at 5°C for up to 12 weeks and that the selection of the appropriate type of PLGA was critical to assuring the stability of the system. The better stability observed when using a PLGA characterized by a 75:25 lactide:glycolide ratio was attributed to<p>its slower degradation rate. Finally, the sustained release of Ab from the developed MS and the preservation of its activity was confirmed in vivo in a pharmacokinetic (pK) study realized in<p>rats. In conclusion, the application of the concept of entrapment into a polymer matrix for<p>stabilization and sustained release of biological compounds was demonstrated through this work.<p><p><p><p>RÉSUMÉ<p><p>Ce projet a pour but de développer un système de délivrance de médicament capable d’augmenter la stabilité et le temps de résidence in vivo des anticorps. Ce système sera administré par voie sous-cutanée et permettra un control précis de la libération du produit et de son niveau plasmatique. Cette plateforme technologique nous permettra de réduire la fréquence d’injection, de réduire potentiellement les effets secondaires et de maintenir des concentrations élevées en anticorps tout en améliorant la vie des patients atteints de maladies chroniques autoimmunes ou inflammatoires. Les formulations à base de polymères synthétiques, biodégradables (PLGA) ont été sélectionnés comme véhicules pour encapsuler les anticorps. Ils offrent en effet une bonne protection pour les anticorps and permettent une libération contrôlée de ceux-ci pendant une période définie. Après l’évaluation de différents méthodes d’encapsulation tels que les procédés d’eau-dans-huile-dans-eau (w/o/w) et solide-dans-huile-dans-eau (s/o/w), l’encapsulation des anticorps sous forme solide apparaissait plus apporpriée pour produire des microsphères de polymère chargées en anticorps. Cette technique nous permettait de maintenir l’anticorps sous sa forme monomérique et d’éviter la formation d’agrégats insolubles qui apparaissaient principalement à l’interface eau/huile. La première partie du projet a été d’optimiser à la fois la méthode nous permettant d’obtenir les anticorps sous forme de particules solides (spray-drying) et la méthode d’encapsulation de ces particules d’anticorps dans les microsphères de polymères. Cela a été réalisé par des plans d’expérience en utilisant une IgG bovine polyclonale comme molécule modèle. Durant l’optimisation du procédé de spray-drying,<p>les solutions aqueuses d’anticorps ont été atomisées en utilisant le mini Spray-Dryer assemblé avec une buse de pulvérisation d’un diamètre de 0.7 mm. En accord avec la taille particulaire (d(0.5) ~5 μm), la stabilité (absence de perte en monomère mesurée par chromatographie d’exclusion de taille et le rendement d’atomisation (> 60 % w/w), les paramètres d’atomisation ont été fixés: 3 mL/min pour le débit de liquide, 130°C /75°C pour la température d’entrée / température de sortie, 800 L/h pour le débit d’air d’atomisation et 30 m3/h pour le débit d’air de séchage. Pour le s/o/w, le dichlorométhane communément utilisé dans les procédés d’encapsulation a été remplacé par l’acétate d’éthyle qui est considéré comme un meilleure solvant organique en terme d’environnement et de sécurité. Les effets de plusieurs paramètres de fabrication ou de formulation ont été évalués sur les propriétés des microsphères polymériques d’anticorps (distribution de taille particulaire, taux de charge en anticorps, stabilité de l’anticorps et efficacité d’encapsulation). Plusieurs paramètres de fabrication et de formulation ont été statistiquement identifiés comme critiques pour obtenir un procédé reproductible (par exemple. La concentration en PLGA, le volume de phase externe, la vitesse d’émulsification et la quantité d’anticorps). La méthode d’encapsulation ainsi optimisée permettait d’obtenir un taux<p>de charge jusqu’à 6% (w/w) avec une efficacité d’encapsulation jusqu’à 60 % (w/w) tout en<p>préservant l’intégrité de l’anticorps encapsulé. Les microsphères produites étaient caractérisées<p>par un d(0.9) inférieur à 110 μm et montraient une libération après 24 h inférieure à 50 % (w/w).<p>Dans le seconde partie du projet, les procédés d’atomisation et d’encapsulation développés avec<p>l’IgG ont été appliqués à un anticorps monoclonal anti-TNF alpha humanisé pour confirmer la<p>conservation de l’activité de l’anticorps pendant ces procédés. La méthode s/o/w sélectionnée<p>permettait de produire des microsphères de PLGA chargées en anticorps avec un profil de libération jusqu’à 6 semaines et un maintien de la stabilité de l’actif. Afin de maintenir l’activité de l’anticorps, à la fois pendant le procédé d’encapsulation et pendant la libération, l’ajout d’un stabilisant tel que le tréhalose est apparu crucial ainsi que le choix du type de PLGA. Il a été démontré que l’utilisation du PLGA caractérisé par un ratio lactide :glycolide de 75 :25 (par exemple, Resomer ® RG755S) diminuait la formation d’espèces de faible poids moléculaire<p>pendant la dissolution. Cela contribuait à préserver l’activité de l’anticorps durant la libération à partir des microsphères. De plus, le profil de libération était modulé en fonction du type de polymère et de sa concentration. Par exemple, l’utilisation d’une solution à 10 % w/v RG755S conduisait à la production de microsphères d’anticorps avec un temps de libération sur 6<p>semaines. L’optimisation de la formulation et du procédé d’encapsulation a permis de produire<p>des microsphères avec des taux de charge en anticorps de maximum 13 % w/w. Il a été démontré<p>que ces microsphères, stockées à 5°C, étaient stables jusqu’à 12 semaines et que la sélection du<p>type de PLGA était critique pour assurer la stabilité du système. La meilleure stabilité a été<p>obtenue en utilisant le PLGA caractérisé par un ratio lactide :glycolide de 75 :25. Cela a été<p>attribué à sa plus faible vitesse de dégradation. Enfin, la libération contrôlée de l’anticorps à<p>partir de ces microsphères et la conservation de son activité ont été confirmées in vivo lors d’une<p>étude pharmacocinétique réalisée chez le rat. En conclusion, ce travail a permis de démontrer<p>l’application du concept d’ « emprisonnement » des composés biologiques dans des matrices<p>polymériques afin de les stabiliser et contrôler leur libération. / Doctorat en Sciences biomédicales et pharmaceutiques / info:eu-repo/semantics/nonPublished